CFD simulation of solids residence time distribution in a multi-compartment fluidized bed

被引:1
|
作者
Zheng Zou [1 ]
Yunlong Zhao [1 ,2 ]
Hu Zhao [1 ,2 ]
Libo Zhang [1 ,2 ]
Zhaohui Xie [1 ]
Hongzhong Li [1 ]
Qingshan Zhu [1 ]
机构
[1] State Key Laboratory of Multi-phase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences
[2] University of Chinese Academy of Sciences
基金
中国国家自然科学基金;
关键词
RTD; Bed geometry; CFD; Hydrodynamics; Fluidization;
D O I
暂无
中图分类号
TQ051.13 [];
学科分类号
080706 ;
摘要
The present work focuses on a numerical investigation of the solids residence time distribution(RTD) and the fluidized structure of a multi-compartment fluidized bed, in which the flow pattern is proved to be close to plug flow by using computational fluid dynamics(CFD) simulations. With the fluidizing gas velocity or the bed outlet height rising, the solids flow out of bed more quickly with a wider spread of residence time and a larger RTD variance(σ2). It is just the heterogeneous fluidized structure that being more prominent with the bed height increasing induces the widely non-uniform RTD. The division of the individual internal circulation into double ones improves the flow pattern to be close to plug flow.
引用
收藏
页码:1706 / 1713
页数:8
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